Nitrification-denitrification via nitrite accumulation for nitrogen removal from wastewaters

被引:162
作者
Ruiz, G
Jeison, D
Rubilar, O
Ciudad, G
Chamy, R
机构
[1] Pontificia Univ Catolica Valparaiso, Sch Biochem Engn, Valparaiso 2340950, Chile
[2] Univ La Frontera, Dept Chem Engn, Temuco 4811230, Chile
关键词
nitrogen removal; nitrite accumulation; nitrite denitrification; oxygen concentration; nitrification-denitrification via nitrite;
D O I
10.1016/j.biortech.2005.02.018
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The biological nitrification-denitrification process is used extensively for removal of ammonia nitrogen from wastewaters. Saves in aeration, organic matter (for denitrification) and surplus sludge are achievable if nitrite accumulation is possible in the nitrification step. In this paper, operational parameters were studied for each process for maximum nitrite accumulation in the nitrification step and nitrite adaptation in the denitrification step. Nitrite accumulation during nitrification can be controlled by the dissolved oxygen (DO) concentration, presenting a maximum of 65% at around 0.7 mg DO/L. Denitrification can be adapted to nitrite and the process is stable if nitrite in the reactor is keep low. The performance of a continuous stirred tank reactor (CSTR) and an up flow sludge blanket reactor (USB) were compared. Once the operational parameters were established, a CSTR for nitrification and an USB reactor for denitrification were operated in series for 25 days. The process was stable and a steady state was maintained for 20 days, and 93.5% of overall nitrogen removal was achieved in the nitrification-denitrification via the nitrite process. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:330 / 335
页数:6
相关论文
共 15 条
[1]  
[Anonymous], 1992, STAND METH EX WAT WA
[2]   Optimal operational factors for nitrite accumulation in batch reactors [J].
Bae, W ;
Baek, S ;
Chung, J ;
Lee, Y .
BIODEGRADATION, 2001, 12 (05) :359-366
[3]  
BLISS P, 1983, BIOL CONTROL NITROBE
[4]   Nitrification at high ammonia loading rates in an activated sludge unit [J].
Campos, JL ;
Garrido-Fernández, J ;
Méndez, R ;
Lema, JM .
BIORESOURCE TECHNOLOGY, 1999, 68 (02) :141-148
[5]   Kinetic models for nitrification inhibition by ammonium and nitrite in a suspended and an immobilised biomass systems [J].
Carrera, J ;
Jubany, I ;
Carvallo, L ;
Chamy, R ;
Lafuente, J .
PROCESS BIOCHEMISTRY, 2004, 39 (09) :1159-1165
[6]   Nitrite reduction by a mixed culture under conditions relevant to shortcut biological nitrogen removal [J].
Chung, JW ;
Bae, W .
BIODEGRADATION, 2002, 13 (03) :163-170
[7]   Partial nitrification of high ammonia concentration wastewater as a part of a shortcut biological nitrogen removal process [J].
Ciudad, G ;
Rubilar, O ;
Muñoz, P ;
Ruiz, G ;
Chamy, R ;
Vergara, C ;
Jeison, D .
PROCESS BIOCHEMISTRY, 2005, 40 (05) :1715-1719
[8]  
JONES WL, 1990, RES J WATER POLLUT C, V62, P259
[9]   Nitrite accumulation by aeration controlled in sequencing batch reactors treating domestic wastewater [J].
Peng, YZ ;
Chen, Y ;
Peng, CY ;
Liu, M ;
Wang, SY ;
Song, XQ ;
Cui, YW .
WATER SCIENCE AND TECHNOLOGY, 2004, 50 (10) :35-43
[10]   Nitrification with high nitrite accumulation for the treatment of wastewater with high ammonia concentration [J].
Ruiz, G ;
Jeison, D ;
Chamy, R .
WATER RESEARCH, 2003, 37 (06) :1371-1377